CN201343475Y - Waste water processing device for regenerated pulp boxboard production - Google Patents
Waste water processing device for regenerated pulp boxboard production Download PDFInfo
- Publication number
- CN201343475Y CN201343475Y CNU2008202108491U CN200820210849U CN201343475Y CN 201343475 Y CN201343475 Y CN 201343475Y CN U2008202108491 U CNU2008202108491 U CN U2008202108491U CN 200820210849 U CN200820210849 U CN 200820210849U CN 201343475 Y CN201343475 Y CN 201343475Y
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- China
- Prior art keywords
- waste water
- tank
- treating waste
- air
- aerobic biochemical
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model relates to a waste water processing device, in particular to a waste water processing device for regenerated pulp boxboard production, which comprises a sedimentation filter tank, a clean water tank, an aerobic biochemical tank, a regulating tank, an air flotation device and a sludge concentration device, wherein the sedimentation filter tank comprises a primary sedimentation filter tank and a secondary sedimentation filter tank; the aerobic biochemical tank comprises a first section aerobic biochemical tank and a second section aerobic biochemical tank; the primary sedimentation filter tank is arranged between the first section aerobic biochemical tank and the second section aerobic biochemical tank; one side of the second section aerobic biochemical tank is provided with the secondary sedimentation filter tank; the clean water tank is connected with aerobic biochemical tank and the air flotation device; and the regulating tank is connected with the air flotation device and the sludge concentration device. The utility model has the mellow and reliable processing technology, and the treated waste water meet the production recycling requirements. The utility model has the advantages of low project investment, low running cost and convenient management. The utility model fully takes the low winter temperature into consideration, the aerobic biochemical tank is arranged under the ground, and a Roots blower is used for supplying oxygen, so the long-time stable running of the system is ensured.
Description
Technical field
The utility model relates to wastewater treatment equipment, refers in particular to a kind of apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production.
Background technology
Present recycled pulp boxboard production equipment, one ton of paper of every production needs clear water 40m
3, to pulverize the deinking sections by waste paper in the technological process wherein and produce waste water, the pulping sections produces waste water, paper machine sections can produce waste water, and original production watering technology ton paper water consumption is too big, has caused the waste of water resources, increased the resource of enterprise and the input of the energy, very uneconomical.Producing back waste water needs a large amount of dischargings, though through handling, natural water is still had more serious pollution.
Summary of the invention
The purpose of this utility model is improved at shortcoming that exists in the background technology and problem, and a kind of energy-saving and environmental protection, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production that cost is low are provided.
System and device of the present utility model comprises sedimentation and filtration ditch, clean water basin, aerobic biochemical pond, equalizing tank, air-floating apparatus, sludge concentration device, wherein sedimentation and filtration ditch comprises one-level sedimentation and filtration ditch, two-stage precipitation filtering basin, the aerobic biochemical pond comprises one section Aerobic Pond and two sections Aerobic Ponds, establish the one-level sedimentation and filtration ditch between one section Aerobic Pond and two sections Aerobic Ponds, two sections Aerobic Pond one sides are established the two-stage precipitation filtering basin; Clean water basin connect aerobic biochemistry pool and air-floating apparatus; Equalizing tank connects air-floating apparatus and sludge concentration device.
Advantage of the present utility model and beneficial effect:
1, treatment process mature and reliable meets production reuse requirement after the wastewater treatment.
2, project investment is low, and running cost is low, is convenient to management.
3, it is lower to fully take into account winter temperature, and biochemistry pool adopts underground, roots blower oxygen supply.
4, the long-time stable operation of assurance system.
Description of drawings
Accompanying drawing is a system and device structure iron of the present utility model
Embodiment
By accompanying drawing as can be known, the utility model comprises sedimentation and filtration ditch, clean water basin 8, aerobic biochemical pond, equalizing tank 7, air-floating apparatus 9, sludge concentration device 10, wherein sedimentation and filtration ditch comprises one-level sedimentation and filtration ditch 1, two-stage precipitation filtering basin 2, the aerobic biochemical pond comprises one section Aerobic Pond 4 and two sections Aerobic Ponds 5, establish 1, two section Aerobic Pond 5 one side of one-level sedimentation and filtration ditch between one section Aerobic Pond 4 and the two sections Aerobic Ponds 5 and establish two-stage precipitation filtering basin 2; Clean water basin 6 connect aerobic biochemistry pool and air-floating apparatus 9; Equalizing tank 7 connects air-floating apparatus 9 and sludge concentration device 10.
One-level sedimentation and filtration ditch 1 described in the utility model and two-stage precipitation filtering basin 2 connect sludge pump 11 for awl bucket spoil disposal structure at the bottom of the pond.Comprise with pipe connection roots blower 12, by roots blower air blast oxygen supply in described one section Aerobic Pond 4 and two sections Aerobic Ponds 5.Described clean water basin 8 comprise reuse water pump 13, are used for connecting the splicer reuse, and reuse water pump 13 is provided with switch valve, and clean water basin 8 are connected to the aerobic biochemical pond.The floating device 9 of described vapour comprises dregs scraper 14, air dissolved pump 15, flocculation agent dispenser 16, coagulant aids dispenser 17, wherein dregs scraper 14 is located at the top of air-floating apparatus 9, air dissolved pump 15 is located at the bottom of air-floating apparatus 9, and flocculation agent dispenser 16 is connected air-floating apparatus 9 and sludge concentration device 10 with coagulant aids dispenser 17.Described sludge concentration device 10 comprises mud concentration tank 18 and sludge dewatering equipment 19, and clear water output is established on mud concentration tank top, and the bottom is established the thickened sludge outlet and connected sludge dewatering equipment 19.Described equalizing tank 7 adopts the form of upward flow sedimentation and filtration, is awl bucket spoil disposal structure at the bottom of the pond, and workshop waste water enters from top, and the bottom connects sludge pump 11.
Technological process of the present utility model and principle:
The waste water of the utility model production plant discharging is all measured homogeneous through oblique net of 200 purposes or the laggard equalizing tank of taper net wheel receipts slurry, and by promoting the pumping shallow air-floatation, equalizing tank also plays the effect of preliminary sedimentation then, and sedimentary mud regularly send concentration basin by sludge pump.The shallow air-floatation technical equipment is used for the floc sedimentation that separating suspension and dosing are separated out.Shallow air-floatation is a kind of advanced person's of reasonable utilization " shallow pool theory " and " zero velocity " principle a quick airfloat equipment, only needs about 3 seconds, and the molten gas concentration of the dissolved air water of its outlet reaches theoretical maximum, and the more common air supporting of molten gas efficient doubles.Because its water-distributing device advanced person can be full for the treatment of pond by ten minutes equably with the full and uniform blended bubble of sewage in advance, nothing " dead band ", " inhomogeneous district ", thus greatly improved purification rate, to paper waste middle section water CODC
CrClearance 60-70%, SS clearance 80%.The catalytic oxidation technology is a kind of aerobic biological film method technology.Be provided with filler in the contact-oxidation pool, the part microorganism grows in filling surface with biomembranous form set, and part then is that cotton-shaped suspension growth is in water.Therefore it has the two characteristics of activated sludge process and biological filter concurrently.
Contact-oxidation pool is established two sections, utilizes the life habit of microorganism to cultivate multiple class dominant microflora, finishes the efficient removal to organic pollutant.Microorganic adhesion bed (filler) is set in each section increases kind and the quantity of microorganism.By filler the bubble that rises is sheared simultaneously, the specific surface area that increases bubble improves oxygen transfer rate.Contact oxidation method is to pollution load BOD
5The sewage that is lower than 30mg/L still has high clearance, and other aerobic process but is difficult to accomplish.The residuum of contact oxidation method is biological demoulding, so sludge output is very low, and surplus sludge volume is less, and dehydration property is good, can reduce the sludge treatment cost.
Mixed solution gravity flow after aerobic enters second pond and carries out the separation of mud liquid, finish denitrification process by returned sluge, the gravity flow of post precipitation supernatant liquor enters clean water basin, and mud is back to the acidication import to improve removal effect by air-lift device, and excess sludge send water extracter to handle.
Clean water basin are actually the water reservoir of enterprise's water of productive use, and the clear water after the processing is directly mended production system by topping-up pump and used.For guaranteeing paper machine quality, behind clean water basin, establish heavy filter tank.Heavy filter tank is designed to the upward flow slag and filters soon, and hybrid reaction dosing facility is housed, and adds flocculation agent and coagulant aids in right amount.Its process characteristic is the filtration velocity height, and water outlet SS content is lower, and filtrate (slag) enterprise can be self-supporting, need not back flushing, and effluent quality is good, and construction is low with running cost, and heavy filter back water quality can satisfy the requirement of paper machine water.Filter back clear liquid is an emission compliance water, and gravity flow enters also paper supply machine use of clear water, residue discharging.
Embodiment described in the utility model only is the description that preferred implementation of the present utility model is carried out; be not that the utility model design and scope are limited; do not breaking away under the preceding topic of the utility model design philosophy; engineering technical personnel make the technical solution of the utility model in this area various modification and improvement; all should fall into protection domain of the present utility model; the technology contents that the utility model is asked for protection all is documented in claims.
Claims (7)
1, a kind of apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production, it is characterized in that system and device comprises sedimentation and filtration ditch, clean water basin (8), aerobic biochemical pond, equalizing tank (7), air-floating apparatus (9), sludge concentration device (10), wherein sedimentation and filtration ditch comprises one-level sedimentation and filtration ditch (1), two-stage precipitation filtering basin (2), the aerobic biochemical pond comprises one section Aerobic Pond (4) and two sections Aerobic Ponds (5), establish one-level sedimentation and filtration ditch (1) between one section Aerobic Pond (4) and the two sections Aerobic Ponds (5), two sections Aerobic Pond (5) one sides are established two-stage precipitation filtering basin (2); Clean water basin (6) connect aerobic biochemistry pool and air-floating apparatus (9); Equalizing tank (7) connects air-floating apparatus (9) and sludge concentration device (10).
2, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1 is characterized in that described one-level sedimentation and filtration ditch (1) and two-stage precipitation filtering basin (2) for awl bucket spoil disposal structure, connect sludge pump (11) at the bottom of the pond.
3, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1 is characterized in that comprising in described one section Aerobic Pond (4) and the two sections Aerobic Ponds (5) with pipe connection roots blower (12), by roots blower air blast oxygen supply.
4, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1, it is characterized in that described clean water basin (8) comprise reuse water pump (13), be used for connecting the splicer reuse, reuse water pump (13) is provided with switch valve, and clean water basin (8) are connected to the aerobic biochemical pond.
5, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1, it is characterized in that described vapour floats device (9) and comprises dregs scraper (14), air dissolved pump (15), flocculation agent dispenser (16), coagulant aids dispenser (17), wherein dregs scraper (14) is located at the top of air-floating apparatus (9), air dissolved pump (15) is located at the bottom of air-floating apparatus (9), and flocculation agent dispenser (16) is connected air-floating apparatus (9) and sludge concentration device (10) with coagulant aids dispenser (17).
6, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1, it is characterized in that described sludge concentration device (10) comprises mud concentration tank (18) and sludge dewatering equipment (19), clear water output is established on mud concentration tank top, and the bottom is established the thickened sludge outlet and connected sludge dewatering equipment (19).
7, apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production according to claim 1, it is characterized in that described equalizing tank (7) adopts the form of upward flow sedimentation and filtration, be awl bucket spoil disposal structure at the bottom of the pond, workshop waste water enters from top, and the bottom connects sludge pump (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202108491U CN201343475Y (en) | 2008-12-10 | 2008-12-10 | Waste water processing device for regenerated pulp boxboard production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202108491U CN201343475Y (en) | 2008-12-10 | 2008-12-10 | Waste water processing device for regenerated pulp boxboard production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201343475Y true CN201343475Y (en) | 2009-11-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202108491U Expired - Fee Related CN201343475Y (en) | 2008-12-10 | 2008-12-10 | Waste water processing device for regenerated pulp boxboard production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201343475Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109629287A (en) * | 2018-12-28 | 2019-04-16 | 江苏理文造纸有限公司 | A method of moisture-proof kraft liner cardboard paper is prepared using wastewater sludge |
-
2008
- 2008-12-10 CN CNU2008202108491U patent/CN201343475Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109629287A (en) * | 2018-12-28 | 2019-04-16 | 江苏理文造纸有限公司 | A method of moisture-proof kraft liner cardboard paper is prepared using wastewater sludge |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091111 Termination date: 20101210 |